US8235098B2 - Heat exchanger flat tube with oblique elongate dimples - Google Patents
Heat exchanger flat tube with oblique elongate dimples Download PDFInfo
- Publication number
- US8235098B2 US8235098B2 US12/019,017 US1901708A US8235098B2 US 8235098 B2 US8235098 B2 US 8235098B2 US 1901708 A US1901708 A US 1901708A US 8235098 B2 US8235098 B2 US 8235098B2
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- dimples
- tube
- elongate
- face
- flat
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- 239000012530 fluid Substances 0.000 description 15
- 239000002826 coolant Substances 0.000 description 14
- 239000000463 material Substances 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000005452 bending Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000005219 brazing Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000009785 tube rolling Methods 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 238000004049 embossing Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 229910001092 metal group alloy Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/42—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/1684—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits having a non-circular cross-section
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/02—Tubular elements of cross-section which is non-circular
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/42—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element
- F28F1/424—Means comprising outside portions integral with inside portions
- F28F1/426—Means comprising outside portions integral with inside portions the outside portions and the inside portions forming parts of complementary shape, e.g. concave and convex
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
- F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
- F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
- F28F3/042—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
- F28F3/044—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element the deformations being pontual, e.g. dimples
Definitions
- the present disclosure generally relates to heat exchangers, and more particularly relates to heat exchangers having a stack of a plurality of flat tubes that each carries a fluid through its interior, with the flat tubes being spaced apart by raised projections or dimples on the flat faces of the tubes, wherein the dimples of one tube contact the dimples of the adjacent tube so as to space the flat faces apart by twice the dimple height.
- flow paths are defined between the spaced-apart flat faces for flow of another fluid so that heat exchange can take place with the fluid flowing through the interiors of the flat tubes.
- a fluid at a relatively high temperature is passed through the interiors of the tubes, a coolant at a lower temperature is passed through the spaces between the tubes, and heat is transferred between the fluids to cool the high-temperature fluid.
- the external dimples are also effective for inducing turbulence in the fluid flowing through the spaces between the adjacent tubes. Accordingly, the dimples are also sometimes referred to as “turbulators” that induce “turbulation” in the fluid flow. Such turbulation can be beneficial for enhancing the heat transfer rate between the fluids, and can also help to prevent boiling of the fluid.
- the dimples are round in plan shape.
- Round dimples provide moderate turbulation, but in many cases a greater degree of turbulation would be desirable.
- top or outermost surfaces of the round dimples that contact each other are relatively small and thus do not provide much stability when stacking the tubes. Accordingly, it is not uncommon for assembly of the tube stack to be faulty because of one tube slipping relative to the adjacent tube such that the dimples “nest”, resulting in too small a spacing between the tubes. Furthermore, because of the small contact areas of the round dimples, even relatively small tolerances on the dimple locations can make it more likely that the dimples will nest. If not corrected, the resulting improper tube spacing would cause undue flow restriction in the coolant and impair proper performance of the heat exchanger.
- the present disclosure relates to a flat tube and a heat exchanger having a stack of a plurality of such flat tubes, wherein a special dimple configuration and arrangement provide enhanced stability for stacking of the tubes.
- the dimples essentially preclude nesting of tubes.
- the dimple configuration and arrangement also provide enhanced turbulation relative to conventional round dimples.
- a flat tube comprises a tube having a first face that is generally flat and an opposite second face that is generally flat, the tube having an interior passage open at opposite first and second ends of the tube for flow of a fluid into one end and out the other end.
- a plurality of spaced-apart dimples are formed on each of the first and second faces.
- At least some of the dimples on each face have an elongate plan shape as viewed perpendicular to the respective face such that each elongate dimple has a length along a major axis greater than a width of the elongate dimple along a minor axis, at least some of the elongate dimples being obliquely oriented with the major axes forming oblique angles with a longitudinal axis of the tube.
- the obliquely oriented elongate dimples are positioned such that when two of the tubes are stacked, the obliquely oriented elongate dimples on opposing faces of the tubes contact one another and the major axes of each contacting pair of elongate dimples are non-parallel to each other.
- Each contacting pair of elongate dimples of adjacent tubes thus forms a “cross” or “X”. It is thought that such elongate dimples can substantially increase the amount of turbulation in the coolant flow.
- crossing elongate dimples provide much larger contact areas than do round dimples, substantially reducing the likelihood of nesting.
- the flat tube also includes orientation indicators comprising projections from each of the first and second faces and each having a height exceeding the height of the dimples but not exceeding twice the height of the dimples.
- the orientation indicators are located on each of the first and second faces of the tube in positions such that when two of the tubes are correctly oriented relative to each other in a tube stack the orientation indicators on the opposing faces of the tubes allow the elongate dimples on the opposing faces to contact one another to space the opposing faces apart by twice the height of the dimples.
- the orientation indicator on one tube contacts the orientation indicator on the other tube and prevents the elongate dimples from contacting each other, thereby indicating improper orientation of the tubes.
- the orientation indicators can be used in a flat tube having the elongate dimples, but are also useful with flat tubes having other dimple configurations such as round dimples. In the case of flat tubes having the above-described obliquely oriented elongate dimples that cross when contacting one another, the orientation indicators prevent the tubes from being stacked in any way other than the proper way in which the elongate dimples contact one another in the crossing manner.
- the orientation indicator on the first face of the tube is positioned proximate to the first end of the tube, and the orientation indicator on the second face is positioned proximate to the second end of the tube.
- Each orientation indicator is positioned to align with a region of the flat face of an adjacent tube that is flat (i.e., where there is no dimple) when the two tubes are properly oriented with respect to each other.
- the elongate dimples are arranged on each face in a two or more rows extending parallel to the longitudinal axis and spaced apart in a width direction of the tube.
- there are three and only three rows of elongate dimples on each face and the elongate dimples in one of the rows (preferably the middle of the three rows) on each face have the major axes oriented substantially parallel to the longitudinal axis of the tube, while the elongate dimples in the other rows on each face have the major axes oriented obliquely to the longitudinal axis.
- the obliquely oriented elongate dimples in one of the rows on each face have the major axes inclined in an opposite direction from the longitudinal axis in comparison to the obliquely oriented elongate dimples in another of the rows.
- the major axes of the obliquely oriented elongate dimples can form an angle relative to the longitudinal axis of about 20° to about 45°.
- the height of the elongate dimples is about 5% to 30% of a thickness of the tube measured between the first face and the second face.
- the length of each elongate dimple is about 10% to about 30% of a width of the tube measured perpendicular to the longitudinal axis between opposite side edges of the tube.
- the present disclosure also relates to a heat exchanger having a shell defining an inner chamber, and a stack of the above-described flat tubes disposed in the inner chamber.
- FIG. 1 is a perspective view, partially broken away to show internal details, of a shell and tube heat exchanger in accordance with the prior art
- FIG. 2 is a perspective view of a flat tube having round dimples in accordance with the prior art
- FIG. 3 is a cross-sectional view through two tubes in the tube stack of the heat exchanger of FIG. 1 , along a plane that is normal to the longitudinal axes of the tubes;
- FIG. 4 is a top elevation of a flat tube in accordance with one embodiment of the invention.
- FIG. 5 is a side elevation of the flat tube of FIG. 4 ;
- FIG. 6 is a bottom elevation of the flat tube of FIG. 4 ;
- FIG. 7 is a magnified fragmentary side elevation of a portion of the flat tube of FIG. 4 ;
- FIG. 8 is magnified fragmentary top elevation of a portion of the flat tube of FIG. 4 ;
- FIG. 9 shows two tubes in accordance with FIG. 4 stacked one on the other
- FIG. 10 is a top elevation of a flat tube in accordance with another embodiment of the invention.
- FIG. 11 is a side elevation of the flat tube of FIG. 10 ;
- FIG. 12 is a bottom elevation of the flat tube of FIG. 10 .
- the present disclosure relates to heat exchangers used for reducing the temperature of a fluid stream passed through the heat exchanger.
- the heat exchangers in accordance with this disclosure can be used with vehicles generally and, more particularly, can be used to cool an exhaust gas stream from an internal combustion engine.
- the heat exchanger configurations of the present disclosure can be used in a variety of different applications.
- FIGS. 1 through 3 show a heat exchanger 30 that does not include the features of the present invention.
- the heat exchanger comprises a stack of elongated, dimpled, flattened tubes that are enclosed in a surrounding shell.
- FIG. 1 illustrates a perspective view of the heat exchanger 30 , sectioned to show the interior of the heat exchanger.
- the heat exchanger 30 comprises a tube stack 31 formed from a plurality of elongated and flattened tubes 38 that are arranged in a stack disposed within a shell 32 .
- a header plate 34 is positioned adjacent both ends of the tube stack 31 , and operates to connect the tubes 38 together adjacent the tube ends, seals the tubes 38 from the coolant, and provides a structure for connecting the tube stack 31 to the shell 32 .
- the shell 32 is configured to surround the tube stack and includes a coolant inlet and a coolant outlet to facilitate passage of a desired cooling fluid or medium therethrough.
- the shell can be formed from suitable structural materials such as metals, metal alloys and the like having desired structural and mechanical properties enabling use in such a heat exchanger application.
- the shell can be formed of a single piece of material.
- the shell 32 is made from a stainless steel material.
- the shell can be made by molding process or by hydroforming or end expanding a seam-welded rectangular tube.
- the shell 32 is configured to surround the tube stack and facilitate a desired degree of coolant circulation therein to provide a desired degree of heat transfer contact with the tube stack.
- the tube stack 31 comprises a plurality of individual flat tubes 38 that are stacked on top of one another.
- each tube 38 in the tube is formed from a single sheet of material that has a pair of edges 38 a and 38 b that extend longitudinally along a length of the tube running between tube ends 39 and 41 .
- the tubes can be formed by bending the sheet of metal into a desired configuration that will provide opposed tube outside surfaces to facilitate stacking and connection with adjacent tubes as better explained below.
- the tube can be formed by bending the metal sheet about itself to provide a central passage defined by a wall structure configuration that has a generally rectangular or flattened oval cross section.
- the edges 38 a and 38 b are positioned adjacent or abutting one other, and are attached to each other to form a seam 38 c that runs lengthwise along the tube.
- the tube is formed in a high-speed tube rolling mill (10 to 100 m/min speed).
- the tube edges 38 a and 38 b are attached to one another by a bonding process such as brazing, welding or the like, and can be attached by TIG or high frequency welding, or can be attached without a welded joint by brazing together.
- the tube 38 can include a flow element 40 disposed therein.
- the flow element 40 can be provided in the form of a corrugated member or the like that extends a partial or complete length of the tube.
- the flow element 40 can be referred to as a fin or a turbulator, and can form a further flow path within the tube, operate to increase the gas or fluid contact surface area within the tube, and operate to increase flow turbulence therein, which can aid in cooling the fluid flowing through the tubes 38 .
- the fin or turbulator can function to add structural rigidity to the tube if desired.
- the tubes 38 are configured each having opposite generally flat faces 42 that include a plurality of projections 43 or dimples extending outwardly therefrom.
- the projections 43 are formed on the faces 42 by a process of stamping, embossing, or the like.
- the projections are provided in the form of dimples, the dimples can either be rolled or stamped into the material in the tube mill prior to the tube radii forming operation.
- the projections 43 are configured having a circular cross section and having a rounded outside surface shape.
- the projections can extend a predetermined distance or height from the tube face, which distance can vary depending on a number of factors such as the type of coolant being passed through the shell, the desired flow rate or residence time for the coolant, and the like.
- the projections can have a height in the range of from about 0.5 mm to 2 mm, and more preferably about 1 mm, wherein the tubes are sized having a length of from about 110 mm to 720 mm, and a width extending between the lengthwise edges in the range of from about 40 mm to 120 mm.
- adjacent tubes 38 are arranged and oriented with one another so that when they are placed in a stacked position, the projections 43 of adjacent tubes 38 make contact with one another.
- This arrangement of tubes with adjacent projections in contact with one another operates to define a plurality of spaces or channels 47 between the outside surfaces of adjacent tubes that can conduct a flow of a coolant therethrough.
- the projections are arranged along the tube surface in a manner that gives rise to a plurality of coolant passages 47 that are configured to influence the passage of coolant through the tube stack in a manner that improves thermal transfer within the heat exchanger.
- the projections 43 of the adjacent tubes can be brazed or welded together in the tube stack. Alternatively, the projections of the adjacent tubes can just be in contact with another without being bonded together.
- FIGS. 4 through 8 A flat tube 100 in accordance with one embodiment of the invention is shown in FIGS. 4 through 8 .
- the tube 100 is similar in overall construction to the tube 38 previously described, differing primarily in terms of the configuration and arrangement of the projections on the opposite flat faces 102 , 104 of the tube. More particularly, the tube 100 includes a plurality of elongate dimples 110 a , 110 b , 110 c (collectively referred to as 110 ) formed on one face 102 , and a plurality of elongate dimples 112 a , 112 b , 112 c (collectively referred to as 112 ) formed on the opposite face 104 .
- Each elongate dimple 110 , 112 has a plan shape, as viewed perpendicular to the respective face 102 , 104 on which it is formed, that is elongate such that a length of the elongate dimple along a major axis A ( FIG. 8 ) is greater than a width of the dimple along a minor axis B.
- the length of the dimple can be at least about 1.5 times the width.
- the dimples 110 , 112 on the tube 100 are configured and arranged such that when two tubes are stacked together with the face 102 of one tube opposing the face 104 of the other, and the tubes are properly oriented and aligned with each other, the elongate dimples 110 on the face 102 contact the elongate dimples 112 on the face 104 .
- the elongate dimples 110 , 112 are oriented with their major axes A oblique with respect to a longitudinal axis of the tube 100 . More specifically, the dimples 110 are arranged in three rows 110 a , 110 b , and 110 c each of which extends parallel to the longitudinal axis of the tube, the rows being spaced apart in the width direction of the tube. The elongate dimples 110 a in the row adjacent one longitudinal side edge of the tube are oriented with their major axes A forming a positive angle + ⁇ relative to the longitudinal axis of the tube.
- the elongate dimples 110 b in the middle row are oriented with their major axes A substantially parallel to the longitudinal axis of the tube.
- the elongate dimples 110 c adjacent the other longitudinal side edge of the tube have their major axes A forming a negative angle ⁇ relative to the longitudinal axis of the tube.
- the elongate dimples 110 a and 110 c are arranged to form a “V” or chevron configuration.
- the elongate dimples 112 on the face 104 are similarly arranged in three rows, with the middle row having elongate dimples 112 b oriented with their major axes parallel to the longitudinal axis of the tube, and the other two rows of elongate dimples 112 a , 112 c having their major axes oriented at positive and negative oblique angles with respect to the longitudinal axis. More specifically, the dimples 110 a are oriented at a negative angle ⁇ and the dimples 110 c are oriented at a positive angle + ⁇ relative to the longitudinal axis. Additionally, the dimples 110 a and 112 a are positioned so that they will contact one another when one tube is stacked with its face 102 opposing the face 104 of the other tube.
- FIG. 9 illustrates two tubes 100 stacked together and shows the upper tube in a transparent fashion so that the dimples on the opposing faces of the tubes are visible.
- the face 104 of each tube faces upwardly and the opposite face 102 of each tube faces downwardly, such that the face 102 of the upper tube opposes the face 104 of the lower tube.
- the dimples 110 a of the upper tube contact the dimples 112 a of the lower tube
- the dimples 110 b of the upper tube contact the dimples 112 b of the lower tube
- the dimples 110 c of the upper tube contact the dimples 112 c of the lower tube.
- Each pair of contacting dimples 110 a , 112 a forms a “cross” or “X” intersection because their major axes are non-parallel to each other.
- each contacting pair of dimples 110 c , 112 c forms a “cross” or “X” intersection.
- the contacting pairs of non-oblique dimples 110 b , 112 b have their major axes parallel to each other and parallel to the longitudinal tube axis.
- the dimples in the middle row could also be oblique, although the illustrated arrangement has symmetry about a longitudinal midline bisecting the tubes into halves, which is thought to be desirable for facilitating a uniform distribution of fluid flow (in the tube width direction) within the passages defined between the faces of the adjacent tubes.
- the crossing pairs of elongate dimples 110 , 112 offer the potential of enhanced turbulation of the coolant flow through the passages between the tubes, relative to conventional round dimples.
- a further advantage of the elongate dimples is a substantially increased amount of contact area between the dimples relative to round dimples. Furthermore, particularly when the dimples are obliquely arranged so they cross each other, the new dimple design provides a substantially reduced sensitivity to positional tolerances of the dimples in terms of the prevention of “nesting” of the dimples of adjacent tubes.
- the oblique elongate dimples as described significantly improve upon round dimples in a number of respects. However, it is still possible (although less likely) for the dimples to nest if the tubes are not properly oriented relative to each other. Furthermore, if the tubes are not properly oriented, the oblique elongate dimples will not cross but rather will be parallel. For example, referring to FIG.
- each tube 100 can include an orientation indicator 120 on the face 102 and a similar orientation indicator 122 on the other face 104 (see FIGS. 4 through 6 ).
- the orientation indicators are projections (similar to dimples) that have a height exceeding the height of the dimples 110 , 112 .
- the height of the orientation indicators preferably is at least about 1.2 times the height of the dimples 110 , 112 , but does not exceed twice the dimple height.
- the orientation indicator 120 on the face 102 is located adjacent one end of the tube 100
- the orientation indicator 122 on the opposite face 104 is located adjacent the opposite end of the tube.
- the orientation indicators can have any suitable shape.
- the orientation indicator 120 on the face 102 is positioned relative to the dimples 112 on the opposite face 104 such that when the tube is stacked with the face 102 opposing the face 104 of another tube, and the two tubes are properly oriented relative to each other, the orientation indicator 120 is aligned with a region of the face 104 that does not have any dimple 112 ; the orientation indicator 122 on the face 104 likewise is positioned so that it is aligned with a region of the opposing face 102 that does not have any dimple 110 (see FIG. 9 ). In this proper orientation, the orientation indicators allow the dimples 110 , 112 to contact each other as already described.
- FIGS. 10 through 12 show a flat tube 200 in accordance with a second embodiment of the invention, having four rows of elongate dimples 210 a , 210 b , 210 c , 210 d on one face 202 , and four rows of elongate dimples 212 a , 212 b , 212 c , 212 d on the opposite face 204 .
- the tube 200 has orientation indicators 220 , 222 respectively located on the faces 202 , 204 in a manner similar to the prior embodiment.
- the two rows of elongate dimples 210 a , 210 b are located on one side of a longitudinal midline of the tube, and the elongate dimples 210 c , 210 d are located on the other side of the longitudinal midline.
- These two groups of rows have the elongate dimples obliquely oriented in opposite directions; more particularly, the dimples 210 a , 210 b are oriented with positive angles (+ ⁇ ), while the dimples 210 c , 210 d are oriented with negative angles ( ⁇ ).
- the dimples 210 a contact the dimples 212 a in a crossing configuration similar to what was described previously, and likewise for the dimple pairs 210 b , 212 b , the pairs 210 c , 212 c , and the pairs 210 d , 212 d.
- the dimples are arranged in straight rows in the longitudinal direction and also in the widthwise or transverse direction of the tube. This arrangement of the dimples in straight rows in the longitudinal direction enables the tube to be made by roll-forming in a tube rolling mill. Alternatively, if the tube is made by other techniques (e.g., stamping of the sheet followed by bending the sheet into a tube shape), then the dimples may be staggered rather than in straight longitudinal rows.
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- Physics & Mathematics (AREA)
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- General Engineering & Computer Science (AREA)
- Geometry (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US12/019,017 US8235098B2 (en) | 2008-01-24 | 2008-01-24 | Heat exchanger flat tube with oblique elongate dimples |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US12/019,017 US8235098B2 (en) | 2008-01-24 | 2008-01-24 | Heat exchanger flat tube with oblique elongate dimples |
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US20090188655A1 US20090188655A1 (en) | 2009-07-30 |
US8235098B2 true US8235098B2 (en) | 2012-08-07 |
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US12/019,017 Active 2031-05-16 US8235098B2 (en) | 2008-01-24 | 2008-01-24 | Heat exchanger flat tube with oblique elongate dimples |
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Cited By (7)
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US20120024510A1 (en) * | 2009-02-05 | 2012-02-02 | Michael Kohl | Heat exchanger, in particular a heating element for motor vehicles |
US20120037346A1 (en) * | 2009-04-20 | 2012-02-16 | Kim Young Mo | Heat exchanger |
US10260821B2 (en) * | 2014-07-30 | 2019-04-16 | T.Rad Co., Ltd. | Flat tube for header-plateless heat exchanger |
US11391523B2 (en) * | 2018-03-23 | 2022-07-19 | Raytheon Technologies Corporation | Asymmetric application of cooling features for a cast plate heat exchanger |
US11421949B2 (en) * | 2017-12-21 | 2022-08-23 | Mahle International Gmbh | Flat tube for an exhaust gas cooler |
US11774179B2 (en) | 2017-06-22 | 2023-10-03 | Rheem Manufacturing Company | Heat exchanger tubes and tube assembly configurations |
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Cited By (8)
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US20120024510A1 (en) * | 2009-02-05 | 2012-02-02 | Michael Kohl | Heat exchanger, in particular a heating element for motor vehicles |
US20120037346A1 (en) * | 2009-04-20 | 2012-02-16 | Kim Young Mo | Heat exchanger |
US9250021B2 (en) * | 2009-04-20 | 2016-02-02 | Kyungdong Navien Co., Ltd. | Heat exchanger |
US10260821B2 (en) * | 2014-07-30 | 2019-04-16 | T.Rad Co., Ltd. | Flat tube for header-plateless heat exchanger |
US11774179B2 (en) | 2017-06-22 | 2023-10-03 | Rheem Manufacturing Company | Heat exchanger tubes and tube assembly configurations |
US11421949B2 (en) * | 2017-12-21 | 2022-08-23 | Mahle International Gmbh | Flat tube for an exhaust gas cooler |
US11391523B2 (en) * | 2018-03-23 | 2022-07-19 | Raytheon Technologies Corporation | Asymmetric application of cooling features for a cast plate heat exchanger |
EP4491992A1 (en) * | 2023-07-13 | 2025-01-15 | Valeo Systemes Thermiques | A flat tube |
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